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WO2020030690A1 - Pvdf à auto-réticulation - Google Patents

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Publication number
WO2020030690A1
WO2020030690A1 PCT/EP2019/071215 EP2019071215W WO2020030690A1 WO 2020030690 A1 WO2020030690 A1 WO 2020030690A1 EP 2019071215 W EP2019071215 W EP 2019071215W WO 2020030690 A1 WO2020030690 A1 WO 2020030690A1
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WO
WIPO (PCT)
Prior art keywords
polymer
moles
monomer
group
recurring units
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/EP2019/071215
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English (en)
Inventor
Julio A. Abusleme
Ségolène BRUSSEAU
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Solvay Specialty Polymers Italy SpA
Original Assignee
Solvay Specialty Polymers Italy SpA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Solvay Specialty Polymers Italy SpA filed Critical Solvay Specialty Polymers Italy SpA
Priority to CN201980055908.3A priority Critical patent/CN112601768B/zh
Priority to KR1020217006594A priority patent/KR102814322B1/ko
Priority to US17/264,954 priority patent/US20210324120A1/en
Priority to EP19748559.2A priority patent/EP3833697B1/fr
Priority to JP2021506278A priority patent/JP7539863B2/ja
Publication of WO2020030690A1 publication Critical patent/WO2020030690A1/fr
Anticipated expiration legal-status Critical
Priority to JP2024061194A priority patent/JP2024105241A/ja
Priority to US18/917,072 priority patent/US20250034300A1/en
Ceased legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
    • C08F214/18—Monomers containing fluorine
    • C08F214/22—Vinylidene fluoride
    • C08F214/225—Vinylidene fluoride with non-fluorinated comonomers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F216/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
    • C08F216/02—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by an alcohol radical
    • C08F216/04—Acyclic compounds
    • C08F216/06—Polyvinyl alcohol ; Vinyl alcohol
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/04—Acids; Metal salts or ammonium salts thereof
    • C08F220/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10—Esters
    • C08F220/20—Esters of polyhydric alcohols or phenols, e.g. 2-hydroxyethyl (meth)acrylate or glycerol mono-(meth)acrylate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F299/00—Macromolecular compounds obtained by interreacting polymers involving only carbon-to-carbon unsaturated bond reactions, in the absence of non-macromolecular monomers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00—Making granules
    • B29B9/02—Making granules by dividing preformed material
    • B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2027/00—Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/12—Use of polyvinylhalogenides or derivatives thereof as moulding material containing fluorine
    • B29K2027/16—PVDF, i.e. polyvinylidene fluoride
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005—Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0014—Catalysts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/24—Condition, form or state of moulded material or of the material to be shaped crosslinked or vulcanised
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2509/00—Use of inorganic materials not provided for in groups B29K2503/00 - B29K2507/00, as filler

Definitions

  • the present invention pertains to crosslinkable vinylidene fluoride
  • PVDFs Polyvinylidene fluoride polymers
  • PVDFs are also used in form of solution, prepared by dissolving PVDF powder in organic solvents like acetone or NMP, for the production of articles such as films, coatings and fibers.
  • the molecular weight of PVDF resins can be increased by crosslinking.
  • Approaches of crosslinking usually involve blending a cross-linker promoter with the fluoropolymer, followed by heat treatment or treatment with ionizing radiation to give crosslinking.
  • US5003008 discloses a method for the preparation of a shaped article of a crosslinked polyvinylidene fluoride resin that comprises the steps of compounding a polyvinylidene fluoride resin with an organosilane, grafting said organosilane compound onto the molecules of the
  • polyvinylidene fluoride resin shaping the resin compound into a form of an article and heating the thus shaped article in the presence of water and a silanol-condensation catalyst in contact therewith.
  • fluorinated copolymers comprising pendant functional groups can be thermally crosslinked in the presence of a cross- linking promoter.
  • EP0969023 discloses functionalized fluoropolymers that may be thermally crosslinked in the presence of cross- linking promoters such as polyamides, wherein the functional groups of said fluoropolymers include esters, alcohols and acids.
  • incorporas in the backbone at least one species of hydrophilic group selected from epoxy group, hydroxyl group, carboxy group, ester group, amide group and acid anhydride group, which is admixed with a plasticizer and a good solvent to prepare a composition useful in the production of porous membranes.
  • the film obtained by extrusion of said composition is then heat treated in order to increase its crystallinity, for the purpose of providing an improved processability of the porous membrane obtained therein. After the heat treatment, the film is subjected to an extraction process to remove the plasticizer and providing the porous membrane.
  • VDF vinylidene fluoride
  • CA carboxyl group-containing vinyl monomer
  • the total amount of monomer (HA) and monomer (CA) in said polymer (F) is of at most 10.0 % by moles, preferably at most 5.0% by moles, more preferably at most 1.5% by moles, with respect to the total moles of recurring units of polymer (F);
  • a second object of the present invention pertains to a composition (C) comprising the crosslinkable polymer (F) as above defined and at least one acidic crosslinking catalyst.
  • a third object of the present invention pertains to a process for preparing a crosslinked fluoropolymer (XLF) comprising the step of submitting a polymer (F) or a composition (C) to a heat treatment at a temperature comprised between 130°C and 250°C.
  • the present invention further pertains to an article comprising the
  • crosslinked fluoropolymer obtained as above defined.
  • the present invention also pertains to a method for making an article
  • XLF crosslinked fluoropolymer
  • step (b) thermally treating the shaped article provided in step (a) at a
  • Suitable hydroxyl group-containing vinyl monomers are compounds of formula (I):
  • Ri, R2 and R3, equal to or different from each other, are independently selected from a hydrogen atom, a halogen atom, and a C1-C3 hydrocarbon group and RO H is a C2-C10 hydrocarbon chain moiety comprising at least one hydroxyl group and possibly containing in the chain one or more oxygen atoms, carbonyl groups or carboxy groups.
  • monomers (HA) are compounds of formula (la):
  • R1, R2 and R3, equal to or different from each other, are independently selected from a hydrogen atom and a C1-C3 hydrocarbon group and R’O H is a C1-C5 hydrocarbon moiety comprising at least one hydroxyl group.
  • Non-limitative examples of monomers (HA) of formula (la) include, notably:
  • HPA 2-hydroxypropyl acrylate
  • the at least one monomer (HA) is hydroxyethyl(meth)acrylate (HEA).
  • Suitable carboxyl group-containing vinyl monomers are compounds of formula (II):
  • Ri, R 2 and R3, equal to or different from each other, are independently selected from a hydrogen atom and a C1-C3 hydrocarbon group and RH is a C1-C10 hydrocarbon chain moiety comprising at least one carboxyl group.
  • monomers (CA) are compounds of formula (Ha):
  • R 1 , R 2 and R3, equal to or different from each other, are independently selected from a hydrogen atom and a C1-C3 hydrocarbon group and R’H is a hydrogen or a C1-C5 hydrocarbon moiety comprising at least one carboxyl group.
  • Non-limitative examples of monomers (CA) of formula (I la) include,
  • the at least one monomer (CA) is acrylic acid (AA).
  • polymer (F) is preferably comprised in the range from 20:1 to 1 :20, preferably from 10:1 to 1 :10, more preferably from 1 :2 to 2:1 ; still more preferably, the molar ratio is 1 :1.
  • polymer (F) It is essential that in polymer (F) a fraction of at least 40% of monomer (HA) and a fraction of at least 40% of monomer (CA) are randomly distributed into said polymer (F).
  • Determination of total average number of (HA) monomer recurring units and of (CA) monomer recurring units in polymer (F) can be performed by any suitable method, NMR being preferred.
  • the fraction of randomly distributed units (HA) and (CA) is preferably of at least 50%, more preferably of at least 60%, most preferably of at least 70 %.
  • Polymer (F) comprises preferably at least 0.1 %, more preferably at least 0.2 % moles of recurring units derived from said monomer (HA).
  • Polymer (F) comprises preferably at most 7.0 %, more preferably at most 5.0 % moles, even more preferably at most 3.0 % moles of recurring units derived from monomer (HA).
  • Polymer (F) comprises preferably at least 0.1 %, more preferably at least 0.2 % moles of recurring units derived from said monomer (CA).
  • Polymer (F) comprises preferably at most 7.0 %, more preferably at most 5.0 % moles, even more preferably at most 3.0 % moles of recurring units derived from monomer (CA).
  • the polymer (F) can be an elastomer or a semi-crystalline polymer
  • the term“semi-crystalline” means a fluoropolymer that has, besides the glass transition temperature Tg, at least one crystalline melting point on DSC analysis.
  • Tg glass transition temperature
  • a semi-crystalline fluoropolymer is hereby intended to denote a
  • fluoropolymer having a heat of fusion of from 10 to 90 J/g, preferably of from 30 to 80 J/g, more preferably of from 35 to 75 J/g, as measured according to ASTM D3418-08.
  • dimethylformamide at 25 °C is lower than 0.80 l/g, preferably lower than 0.50 l/g, more preferably lower than 0.20 l/g.
  • the polymer (F) of the present invention usually has a melting temperature (Tm) comprised in the range from 130 to 200°C.
  • the melting temperature may be determined from a DSC curve obtained by differential scanning calorimetry (hereinafter, also referred to as DSC).
  • the melting temperature (Tm) is determined on the basis of the peak having the largest peak area.
  • the heat treatment step of the process invention is carried out in an oven, which may contain air or an inert gas enveloping the article.
  • the polymer (F) may further comprise recurring units derived from one or more fluorinated comonomers (CF) different from VDF.
  • fluorinated comonomer CF
  • fluorinated comonomer CF
  • Non-limitative examples of suitable fluorinated comonomers include, notably, the followings: (a) C2-C8 fluoro- and/or perfluoroolefins such as tetrafluoroethylene (TFE), hexafluoropropylene (HFP), pentafluoropropylene and
  • chloro- and/or bromo- and/or iodo-C2-C6 fluoroolefins such as chlorotrifluoroethylene (CTFE).
  • the fluorinated comonomer (CF) is preferably HFP.
  • polymer (F) is semi-crystalline and
  • the polymer (F) more preferably comprises recurring units derived from:
  • VDF vinylidene fluoride
  • HA hydroxyl group-containing vinyl monomer
  • CA carboxyl group-containing vinyl monomer
  • CF fluorinated comonomer
  • the polymer (F) may be obtained by polymerization of a VDF monomer, at least one monomer (HA), at least one monomer (CA) and optionally at least one comonomer (CF), either in suspension in organic medium, according to the procedures described, for example, in WO 2008129041 , or in aqueous emulsion, typically carried out as described in the art (see e.g. US 4,016,345, US 4,725,644 and US 6,479,591).
  • the procedure for preparing the polymer (F) comprises polymerizing in an aqueous medium in the presence of a radical initiator the vinylidene fluoride (VDF) monomer, monomer (FIA) and monomer (CA), and optionally comonomer (CF), in a reaction vessel, said process comprising
  • pressure is maintained above critical pressure of vinylidene fluoride.
  • the pressure is maintained at a value of more than 50 bars, preferably of more than 75 bars, even more preferably of more than 100 bars.
  • continuous feeding means that slow, small, incremental additions the aqueous solution of monomer (HA) and monomer (CA) take place until polymerization has concluded.
  • the aqueous solution of monomer (HA) and monomer (CA) continuously fed during polymerization amounts for at least 50 % wt of the total amount of monomer (HA) and monomer (CA) supplied during the reaction (i.e. initial charge plus continuous feed).
  • % wt the total amount of monomer (HA) and monomer (CA) supplied during the reaction
  • at least 60 % wt, more preferably at least 70 % wt, most preferably at least 80 % wt of the total amount of monomer (HA) and monomer (CA) is continuously fed during polymerization.
  • An incremental addition of VDF monomer can be effected during polymerization, even if this requirement is not mandatory.
  • the process of the invention is carried out at a temperature of at least 35°C, preferably of at least 40°C, more preferably of at least 45°C.
  • polymer (F) is typically provided in form of powder.
  • polymer (F) is typically provided in the form of an aqueous dispersion (D), which may be used as directly obtained by the emulsion polymerization or after a concentration step.
  • aqueous dispersion (D) preferably, the solid content of polymer (F) in dispersion (D) is in the range comprised between 20 and 50% by weight.
  • Polymer (F) obtained by emulsion polymerization can be isolated from the aqueous dispersion (D) by concentration and/or coagulation of the dispersion and obtained in powder form by subsequent drying.
  • Polymer (F) in the form of powder may be optionally further extruded to provide polymer (F) in the form of pellets.
  • Extrusion is suitably carried out in an extruder. Duration of extrusion
  • the polymer (F) may be dissolved in any suitable organic solvent to
  • solution (S) of polymer (F) Preferably, the solid content of polymer (F) in solution (S) is in the range comprised between 2 and 30% by weight.
  • Non-limitative examples of suitable organic solvents for dissolving polymer (F) are N-methyl-2-pyrrolidone (NMP), N,N-dimethylformamide, N,N- dimethylacetamide, dimethylsulfoxide, hexamethylphosphamide, dioxane, tetrahydrofuran, tetramethylurea, triethyl phosphate, and trimethyl phosphate, aliphatic ketones, cycloaliphatic ketones, cycloaliphatic esters. These organic solvents may be used singly or in mixture of two or more species.
  • Polymer (F) can be shaped into an article before exposure to thermal treatment and crosslinking.
  • the crosslinking process can be coordinated with the manufacturing of the polymer (F) into a shaped article.
  • Polymer (F) may be thermally heated to undergo crosslinking as it is or in composition with an acidic crosslinking catalyst.
  • a further object of the present invention is thus a composition (C) comprising the crosslinkable polymer (F) as above defined and at least one acidic crosslinking catalyst.
  • Suitable acidic crosslinking catalysts include, for example, Lewis acids, strong mineral acids, e.g., sulfuric acid, phosphoric acid, polyphosphoric acid, perchloric acid, and the like; saturated aliphatic hydrocarbon sulfonic acids and the aromatic hydrocarbon sulfonic acids, e.g., ethanesulfonic acid, propanesulfonic acid, benzenesulfonic acid, toluenesulfonic acid, naphthalenesulfonic acid, lower alkyl substituted benzenesulfonic acid, and the like.
  • Lewis acids strong mineral acids, e.g., sulfuric acid, phosphoric acid, polyphosphoric acid, perchloric acid, and the like
  • saturated aliphatic hydrocarbon sulfonic acids and the aromatic hydrocarbon sulfonic acids e.g., ethanesulfonic acid, propanesulfonic acid, benzenesulfonic acid, toluenes
  • Suitable Lewis acids are inorganic or organic metal compounds in which the cation is preferably selected from the group consisting of boron, aluminium, tin, antimony and iron.
  • Lewis acids e.g., boron trifluoride, aluminum chloride, zinc chloride, stannous chloride, antimony trichloride, ferric chloride, boron trifluoridedimethyl ether complex, boron trifluoride-diethyl ether complex, boron trifluoride-dipropyl ether complex, and the like, with stannous chloride being particularly preferred.
  • metal halide Lewis acids e.g., boron trifluoride, aluminum chloride, zinc chloride, stannous chloride, antimony trichloride, ferric chloride, boron trifluoridedimethyl ether complex, boron trifluoride-diethyl ether complex, boron trifluoride-dipropyl ether complex, and the like, with stannous chloride being particularly preferred.
  • the Lewis acids include not only Lewis acids themselves but also metals or metal compounds which impart a function of Lewis acid, for example oxides and sulfides, antimony trioxide (Sb 2 03), zinc oxide (ZnO), and zinc sulphide (ZnS) being preferred.
  • composition (C) the acidic crosslinking agent is preferably comprised in an amount comprised between 0.001 and 2.0% by weight, more preferably comprised between 0.005 and 0.5% by weight with respect to the total weight of polymer (F).
  • composition (C) is obtained by mixing the acidic
  • crosslinking agent with polymer (F) in a suitable mixer.
  • Composition (C) may be obtained by mixing the acidic crosslinking agent with polymer (F) in the form of solution (S), as above defined, leading to a composition (CS) in the form of solution.
  • Composition (C) may be obtained mixing the acidic crosslinking agent with polymer (F) in the form of dispersion (D), as above defined, leading to a composition (CD) in the form of dispersion.
  • composition (C) comprises, preferably consists of:
  • VDF vinylidene fluoride
  • HA hydroxyl group-containing vinyl monomer
  • CA carboxyl group-containing vinyl monomer
  • an acidic crosslinking catalyst in an amount comprised between 0.001 and 2.0% by weight, more preferably comprised between 0.005 and 0.5% by weight with respect to the total weight of polymer (F).
  • composition (CS) [0086] In another embodiment of the present invention, a composition (CS)
  • VDF vinylidene fluoride
  • HA hydroxyl group-containing vinyl monomer
  • CA carboxyl group- containing vinyl monomer
  • CF fluorinated comonomer
  • an acidic crosslinking catalyst in an amount comprised between 0.001 and 2.0% by weight, more preferably comprised between 0.005 and 0.5% by weight with respect to the total weight of polymer (F); and c) at least one organic solvent.
  • VDF vinylidene fluoride
  • HA hydroxyl group-containing vinyl monomer
  • CA carboxyl group-containing vinyl monomer
  • composition (CS) and composition (CD) can be submitted to a heat
  • the crosslinkable polymer (F) or composition (C) of the present invention may be thermally treated at a temperature comprised between 130°C and 250°C to achieve a crosslinked fluoropolymer (XLF) characterized by an enhanced molecular weight.
  • XLF crosslinked fluoropolymer
  • thermal treatment As used herein, “thermal treatment”,“thermally crosslinked” and “occurs thermally” are understood to mean that the cross-linking process of the invention is activated by temperature.
  • time required to achieve cross-linking will in general depend on the temperature, with cross-linking occurring more rapidly as temperature increases.
  • the time of the heat treatment may thus vary from 5 minutes up to 30 days, depending on the temperature and on the nature of polymer (F).
  • Thermal crosslinking involves reaction of at least a portion of the hydroxyl groups of recurring units derived from monomer (HA) with at least a portion of the carboxyl groups of recurring units derived from monomer (CA).
  • the polymer (F) and the composition (C) of the invention can be suitably converted into shaped articles and then submitted to thermal crosslinking to improve the performances of said articles.
  • the present invention provides a method for making an article comprising the crosslinked fluoropolymer (XLF), the method comprising:
  • step b) thermally treating the shaped article obtained in step a) at a
  • dimethylformamide at 25 °C is comprised between 0.05 l/g and 0.15 l/g.
  • the present invention provides a method for making an article comprising the crosslinked fluoropolymer (XLF), the method comprising:
  • step b) thermally treating the shaped article obtained in step b) at a
  • dimethylformamide at 25°C is suitably comprised between 0.15 l/g and 0.35 l/g.
  • the present invention provides a method for making an article comprising the crosslinked fluoropolymer (XLF), the method comprising:
  • composition (C) composition (C)
  • step b thermally treating the shaped article obtained in step b at a
  • the present invention further pertains to an article comprising the
  • crosslinked fluoropolymer obtained as above defined.
  • compositions (C) comprising said polymers (F) are for the manufacture of articles that can be shaped and later undergo crosslinking by thermal treatments, while maintaining the well known and proved characteristics of PVDF in terms of chemical resistance, surface properties, high service temperatures.
  • polymers (F) or compositions (C) in solid form are examples.
  • Polymers (F) or compositions (C) in solution are particularly suitable for the preparation of film and membranes, porous membranes in particular such as for example as described in Journal of Membrane Science 178 (2000) 13-23.
  • Polymers (F) or compositions (C) in dispersion are particularly suitable for the preparation of components for batteries, such as binders for electrodes and layers to be used as separator coating, such as for example for applications described in US201503906 (ARKEMA Inc.) 19/08/2014.
  • binders for electrodes and layers to be used as separator coating such as for example for applications described in US201503906 (ARKEMA Inc.) 19/08/2014.
  • Intrinsic viscosity (h) [dl/g] was measured using the following equation on the basis of dropping time, at 25°C, of a solution obtained by dissolving the polymer (F) in N,N-dimethylformamide at a concentration of about 0.2 g/dl using a Ubbelhode viscosimeter:
  • h G is the relative viscosity, i.e. the ratio between the dropping time of sample solution and the dropping time of solvent
  • sp is the specific viscosity, i.e. h G -1
  • G is an experimental factor, which for polymer (F) corresponds to 3.
  • Comp 1 VDF-AA copolymer prepared according to WO 2008129041.
  • Comp 2 VDF-HEA copolymer prepared according to WO 2008129041.
  • Example 1 Preparation of tetrapolymer VDF-HFP-AA-HEA (Copo 3)
  • HFP hexafluoropropylene
  • VDF vinylidene fluoride
  • Example 2 Preparation of terpolymers : VDF-AA-HEA (F1 , F2, F3)
  • Polymers F2 and F3 and the pressure was fixed at 110 bar.
  • the pressure was kept constantly equal to 110 bar by feeding during the polymerization, the acrylic acid and the hydroxyethyl acrylate mixed in aqueous solution with a concentration of AA and HEA as described in the table 1. After this feeding, no more aqueous solution was introduced and the pressure started to decrease.
  • the polymerization was stopped by degassing the reactor until reaching atmospheric pressure. A conversion of monomers between 77 and 79% were reached.
  • the polymer so obtained was then recovered, washed with demineralised water and dried at 65°C during all the night.
  • Example 3 Preparation of tetrapolymers: VDF-HFP-AA-HEA (F4, F5, F6, F7)
  • the acrylic acid (AA) and the hydroxyethyl acrylate (HEA) were introduced, see Table 2.
  • HFP hexafluoropropylene
  • VDF vinylidene fluoride
  • the reactor was gradually heated until a set- point temperature at 57°C and the pressure was fixed at 110 bar.
  • the pressure was kept constantly equal to 110 bar by feeding during the polymerization, the acrylic acid and the hydroxyethyl acrylate mixed in aqueous solution with a concentration of AA and HEA as described in the table 2.
  • no more aqueous solution was introduced and the pressure started to decrease.
  • the polymerization was stopped by degassing the reactor until reaching atmospheric pressure. A conversion of monomers between 72 and 76% was reached.
  • the polymer so obtained was then recovered, washed with demineralised water and dried at 65°C during all the night.
  • the fraction of randomly distributed units (HA) and (CA) is more than 40% for polymers F1 to F6.
  • Polymer F6 obtained in Example 3 was pelletized in a twin screw co- rotating extruder (Leistritz LSM 30.34 GG-5R having a screw diameter D of 34 mm) equipped with a main feeder. There is six temperature controlled zones that permit to set the desired temperature profile (see Table 4).
  • the die was composed of two holes having each a diameter of 4mm.
  • the extruder rotation speed was 100 rpm.
  • the two extrudates were cooled in a water tank, pull out and then dried with compressed air. At the end, the two extrudates were cut-off in order to obtain the pellets.
  • Example 5 Compounding with Sb203 (100 ppm), melt extrusion and
  • Example 6 Compounding with Sb203 (250 ppm), melt extrusion and
  • Example 3 the Polymer F6 obtained in Example 3 was mixed with a high speed mixer Henschel (FML 40 Model) with 0.025 weight percent of Antimony(lll) oxide (Sb 2 03) provided by Sigma-Aldrich with respect to the weight of polymer F6. Then, in a second step, the mixed powder was introduced and pelletized in a twin screw co-rotating extruder (Leistritz LSM 30.34 GG-5R having a screw diameter D of 34 mm) equipped with a main feeder. The same six temperature controlled zones in Example 4 were used (see Table 4). The die was composed of two holes having each a diameter of 4mm. The extruder rotation speed was 100 rpm. The two extrudates were cooled in a water tank, pull out and then dried with compressed air. At the end, the two extrudates were cut-off in order to obtain the pellets.
  • a twin screw co-rotating extruder Leistritz LSM 30.34 GG-5R having a screw diameter D of 34
  • Example 7 Compounding with ZnO (250 ppm), melt extrusion and
  • Example 8 Compounding with ZnO (10000 ppm), melt extrusion and
  • Example 9 Compounding with ZnS (10000 ppm), melt extrusion and
  • Example 10 heat treatment - crosslinking
  • Example 4 With the pellets of Example 4 and Example 6 two plaques each of 1.5mm of thickness (10x10cm) were prepared. One of each has been treated in an oven at 140°C and 48h. Then percentage of gel of the four plaques was determined as follows.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

La présente invention concerne des copolymères de fluorure de vinylidène réticulables comprenant des unités récurrentes dérivées de monomères hydrophiles utiles pour produire des articles façonnés caractérisés par des performances améliorées.
PCT/EP2019/071215 2018-08-09 2019-08-07 Pvdf à auto-réticulation Ceased WO2020030690A1 (fr)

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CN201980055908.3A CN112601768B (zh) 2018-08-09 2019-08-07 自交联pvdf
KR1020217006594A KR102814322B1 (ko) 2018-08-09 2019-08-07 자가 가교결합 pvdf
US17/264,954 US20210324120A1 (en) 2018-08-09 2019-08-07 Self crosslinking pvdf
EP19748559.2A EP3833697B1 (fr) 2018-08-09 2019-08-07 Pvdf à auto-réticulation
JP2021506278A JP7539863B2 (ja) 2018-08-09 2019-08-07 自己架橋ｐｖｄｆ
JP2024061194A JP2024105241A (ja) 2018-08-09 2024-04-05 自己架橋ｐｖｄｆ
US18/917,072 US20250034300A1 (en) 2018-08-09 2024-10-16 Self crosslinking pvdf

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CN119039506A (zh) * 2023-05-29 2024-11-29 宁德时代新能源科技股份有限公司 含氟聚合物、制备方法、负极浆料、负极极片、二次电池及用电装置

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Publication number Priority date Publication date Assignee Title
WO2023132373A1 (fr) * 2022-01-10 2023-07-13 ダイキン工業株式会社 Dispersion aqueuse, composition de revêtement, film de revêtement et article revêtu
JPWO2023132373A1 (fr) * 2022-01-10 2023-07-13

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JP7539863B2 (ja) 2024-08-26
JP2024105241A (ja) 2024-08-06
CN112601768B (zh) 2023-01-13
KR102814322B1 (ko) 2025-05-30
KR20210042127A (ko) 2021-04-16
EP3833697A1 (fr) 2021-06-16
US20250034300A1 (en) 2025-01-30
CN112601768A (zh) 2021-04-02

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